BACKGROUND OF THE INVENTION
(a) Field of the Invention
[0001] The present invention relates to a manufacturing method of a lithium-titanium composite
oxide doped with different metals, and to a lithium-titanium composite oxide doped
with two kinds of different metals. More particularly, the present invention relates
to a manufacturing method of a lithium-titanium composite oxide doped with different
metals after adjusting a mixing ratio of two kinds of different metals, solid-phase
mixing them, pulverizing the same, and spray drying the same to adjust contents of
impurities, and a lithium-titanium composite oxide doped with different metals manufactured
therefrom.
(b) Description of the Related Art
[0002] A non-aqueous electrolyte battery charged and discharged by lithium ions moving between
negative and positive electrodes is actively researched and developed as a high energy
density battery. Recently, a lithium-titanium composite oxide having a high Li intercalation/deintercalation
potential has drawn attention. Since lithium metal is not extracted from the lithium-titanium
composite oxide during lithium intercalation/deintercalation, the lithium-titanium
composite oxide has an advantage of rapid charge and excellent low temperature performance.
[0003] This lithium-titanium composite oxide includes spinel-type lithium titanate represented
by a general formula Li (
1+x)Ti (
2-x)O
y (x = -0.2 to 1.0 and y = 3 to 4) and may be, for example, Li
4/3Ti
5/3O4, LiTi
2O
4, or Li
2TiO
3. This material has been conventionally used as a positive active material and may
be used as a negative active material, and thus is much expected to continue to be
used as a positive and negative electrode active material. This material has a voltage
of 1.5 V with a reference to lithium and a long cycle-life. In addition, since expansion
and contraction of the material is negligible during the charge-discharge, this material
garners attention as an electrode material when a large-scale battery is manufactured.
In particular, the spinel-type lithium titanate (represented by Li
4+xTi
5O
12 (0 ≤ x ≤ 3)) has a small volume change during the charge and discharge and excellent
reversibility, and thus receives attention.
[0004] However, the spinel-type lithium titanate has theoretical capacity of 175 mAh/g and
thus has a limit in terms of high capacity. In addition, the spinel-type lithium titanate
is partially phase-separated into rutile-type TiO
2 (r-TiO
2) during the manufacturing process.
[0005] The rutile-type TiO
2 (r-TiO
2) has a rock salt structure, and thus has electrochemical activity, but a problem
of deteriorating effective capacity of the lithium-titanium composite oxide obtained
therefrom due to a low reaction speed, an inclined potential curve, and small capacity
occurs.
SUMMARY OF THE INVENTION
[0006] In order to solve the problems of the prior arts, the present invention provides
a manufacturing method of a lithium-titanium composite oxide having improved initial
capacity and rate capability by doping different metals, suppressing generation of
anatase and rutile-type titanium dioxide, and controlling sizes of primary particles,
and a lithium-titanium composite oxide doped with different metals manufactured by
the method.
[0007] In order to achieve the purpose, the present invention provides a manufacturing method
of a lithium-titanium composite oxide doped with different metals that includes:
- i) solid-phase mixing a lithium-containing compound, a titanium oxide, a different
metal M-containing compound, and a different metal A-containing compound stoichiometrically;
- ii) dispersing the solid-phase mixture of i) in a solvent and wet-pulverizing the
mixture to provide particles having an average particle diameter of 0.3 µm to 0.8
µm to prepare a slurry;
- iii) spray-drying the slurry to provide particles; and
- iv) firing the spray-dried particles to manufacture a lithium-titanium composite oxide
doped with different metals represented by the following chemical formula.
[Chemical Formula] Li4Ti5-(x+y)MxAyO12
(In the chemical formula, the M is selected from the group consisting of Zr, Mg, Al,
Ni, Co, Mn, and Cu, the A is selected from the group consisting of Na, K, V, and B,
0.1≤x≤1.5, 0≤y≤1, x+y≤2, and 8≤x/y≤9)
[0008] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, the different metal M is Zr, and the different metal
A is Na.
[0009] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, the Na-containing compound is selected from the group
consisting of sodium carbonate, sodium hydroxide, or sodium carbonate and sodium hydroxide,
and sodium hydroxide is preferable because it dissolves in a wet process.
[0010] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, the Zr-containing compound is Zr(OH)
4, ZrO
2, or a mixture thereof.
[0011] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, the titanium oxide is an anatase-type or titanium
oxide hydrate.
[0012] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, the lithium-containing compound is lithium hydroxide
or lithium carbonate.
[0013] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, in the ii) process, water is used for a solvent,
and the wet-pulverizing is performed using zirconia beads at 2000 to 4000 rpm.
[0014] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, in the iii) process, the spray drying is performed
while inflowing hot air at a temperature of 250 to 300 °C and discharging hot air
at a temperature of 100 to 150 °C.
[0015] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, in the iv) process, the firing is performed by firing
the spray-dried resultant of the iii) process under an air atmosphere at 700 to 800
°C for 5 h to 10 h.
[0016] In the manufacturing method of a lithium-titanium composite oxide doped with different
metals of the present invention, the method further includes v) pulverizing the fired
particles in the iv) process. In the present invention, a dry pulverizing method of
the lithium-titanium composite oxide is not particularly limited, but the particles
formed by the firing process are preferably pulverized to a microsize, specifically
using a jet air mill.
[0017] The present invention provides a lithium-titanium composite oxide doped with two
kinds of different metals that is manufactured by the dry pulverizing method, represented
by the chemical formula, having a spinel structure, and including secondary particles
formed by aggregating primary particles, wherein a diameter of the primary particles
ranges from 0.2 µm to 0.6 µm and a diameter of the secondary particles ranges from
5 µm to 25 µm.
[Chemical Formula] Li
4Ti
5-(x+y)M
xA
yO
12
(In the chemical formula, the M is selected from the group consisting of Zr, Mg, Al,
Ni, Co, Mn, and Cu, the A is selected from the group consisting of Na, K, V, and B,
0.1≤x≤1.5, 0≤y<1, x+y≤2, and 8≤x/y≤9)
[0018] The lithium-titanium composite oxide doped with two kinds of different metals of
the present invention has a main peak intensity of anatase-type TiO
2 of less than or equal to 1, a main peak intensity of R-TiO
2 of less than or equal to 1, and a main peak intensity of Li
2TiO
3 of less than or equal to 5 when a main peak intensity of Li
4/3Ti
5/3O
4 is 100.
[0019] The present invention provides a positive electrode including the lithium-titanium
composite oxide doped with different metals of the present invention as a positive
active material, or a negative electrode including the lithium-titanium composite
oxide doped with different metals of the present invention as a negative active material.
[0020] The present invention provides a rechargeable lithium battery including a positive
electrode including the lithium-titanium composite oxide doped with different metals
of the present invention as a positive active material, or a rechargeable lithium
battery including a negative electrode including the lithium-titanium composite oxide
doped with different metals of the present invention as a negative active material.
[0021] Hereinafter, the present invention is described in detail.
[0022] The present invention provides a method of manufacturing the lithium-titanium composite
oxide by simultaneously solid-phase mixing a lithium compound and a titanium compound
as raw compounds and a different metal-containing compound for doping the raw compound
with two kinds of different metals, and adjusting a ratio of the two kinds of different
metals-containing compounds.
[0023] The titanium oxide-containing compound as a starting material may be any of a chloride,
a sulfate, an organic salt, and the like. However, the titanium oxide-containing compound
as a starting material may have a crystal structure such as anatase-type titanium
dioxide or titanium oxide hydrate in order to manufacture a lithium-titanium composite
oxide having excellent discharge capacity or battery characteristics as starting materials.
[0024] The anatase-type titanium dioxide needs to have purity of greater than or equal to
95 %, or greater than or equal to 98 %. When the purity is less than 95 %, capacity
per weight of an active material is deteriorated. For example, the anatase-type titanium
dioxide having high purity of 99.99 % may be used, but it is expensive. When the anatase-type
titanium dioxide has purity of greater than or equal to 98 %, the influence of high
purity in terms of an electrode active material becomes smaller than an influence
on a particle diameter and a particle shape.
[0025] In the lithium compound in the manufacturing method of the present invention, a starting
material may be a lithium salt such as lithium hydroxide, lithium hydroxide monohydrate,
lithium oxide, lithium hydrogen carbonate, or lithium carbonate.
[0026] In the manufacturing method of the present invention, the different metal M of the
doped two kinds of different metals is selected from the group consisting of Zr, Mg,
Al, Ni, Co, Mn, and Cu, while the different metal A is selected from the group consisting
of Na, K, V, and B, and it is preferable that Zr and Na are simultaneously doped in
terms of capacity characteristics and structural characteristics.
[0027] The Na-containing compound is preferably sodium hydroxide, sodium carbonate, or a
mixture thereof. The Zr-containing compound is preferably Zr(OH)
4, ZrO
2, or a mixture thereof.
[0028] In the present invention, the different metal M may be doped in an amount of greater
than or equal to 0.1 % and less than or equal to 1.5 %, while the different metal
A may be doped in a range of 0 % to 1 %, and herein, the different metal M and the
different metal A may be doped in a total amount of less than or equal to 2 % and
in a ratio of the doping amount x of the different metal M relative to the doping
amount y of the different metal A satisfying 8≤ x/y ≤9.
[0029] When the different metal M is doped in an amount of greater than 1.5 %, conductivity
may be rather deteriorated, and overall performance of a battery may be deteriorated,
and when the different metal A is doped in an amount of 0 wt%, an effect of improving
battery safety due to doping of the different metals may be insignificant.
[0030] The method of a lithium-titanium composite oxide according to the present invention
provides an assembled powder of a secondary particle formed by aggregation of primary
particles by mixing a lithium compound, a titanium compound, and a doping metal as
starting materials stoichiometrically, dispersing a solid-phase mixture in a liquid
medium, wet-pulverizing to prepare a slurry and spray-drying the slurry and firing
the resultant using a known method.
[0031] In the manufacturing method of the present invention, the simultaneously-mixed lithium
compound, titanium compound, and doping metal are dispersed in a dispersion medium
and then wet-pulverized by using a medium-stirring type of grinder and the like. The
dispersion medium used for wet-pulverizing slurry may be various organic solvents
and aqueous solvents, but specifically may be water. The raw compounds may be used
in an amount of greater than or equal to 50 wt% and less than or equal to 60 wt% based
on the total weight of the slurry. When the weight ratio is less than the range, the
slurry has an extremely thin concentration, and spherically-shaped particles obtained
through the spray-drying may become unnecessarily small or be easily broken. When
the weight ratio is greater than the range, it may be difficult to maintain uniformity
of the slurry.
[0032] The wet-pulverization may be performed at 2000 to 4000 rpm, so that a solid in the
slurry may have an average particle diameter (D50) ranging from 0.3 µm to 0.8 µm.
When the solid in the slurry has too large an average particle diameter, sphericity
as well as reactivity may be deteriorated during the firing process, and thus charge
density of a final powder tends to be deteriorated. However, when the slurry is more
than necessarily pulverized, the pulverization cost is increased, and thus the slurry
may be wet-pulverized until the average particle diameter ranges from 0.3 µm to 0.8
µm.
[0033] Then, the lithium-titanium composite oxide powder of the present invention may be
spray-dried to bond primary particles and form secondary particles, and herein, the
primary particles may have a diameter ranging from 0.3 µm to 0.7 µm and the secondary
particles may have a diameter ranging from 5 µm to 25 µm.
[0034] The spraying may be performed by pressing a nozzle having a predetermined hole size
but using any commonly-used spray-drying equipment without a particular limit. In
general, a sprayer is classified into a rotating disc type and a nozzle type, and
the nozzle type of sprayer is classified into a pressure nozzle and a two-fluid nozzle.
In addition, the sprayer may include any well-known equipment in a related field such
as a rotary sprayer, a pressure nozzle, an air nozzle, a sonic nozzle, and the like.
The spray equipment may be selected typically considering a supply speed, viscosity
of a supply, a desired particle size of a spray-dried product, dispersion, a droplet
size of a water-in-oil emulsion or a water-in-oil microemulsion, and the like.
[0035] In the step iii) of spray-drying the slurry of the step ii), a charge hot air temperature
may be set at about to 250 to 300 °C, while a discharge hot air temperature may be
set at 100 to 150 °C to improve a particle shape, a particle size, and crystallinity.
[0036] Then, a mixed powder obtained in this way is fired. The firing may be performed at
greater than or equal to 600 °C, greater than or equal to 700 °C, in general greater
than or equal to 900 °C, but specifically, greater than or equal to 800 °C depending
on a kind of lithium compound and titanium oxide, metal compound such as different
metals and the like, and the like, as a raw compound. Herein, the firing may be controlled
depending on the composition of the raw compound, but when performed at too high a
temperature, a primary particle may overgrow, while when performed at too low a temperature,
volume density becomes small, and a specific surface area becomes extremely large.
[0037] The firing may be performed for different times depending on a temperature, but for
greater than or equal to 30 min, greater than or equal to 5 h, but commonly greater
than or equal to 20 h, and specifically, less than or equal to 10 h within the aforementioned
temperature range. When the firing is performed for too short a time, a lithium-titanium
composite oxide powder having excellent crystallinity is difficult to obtain, while
when performed for too long a time, it is not p[particularly practical. In addition,
when performed for too long a time, the lithium-titanium composite oxide powder needs
to be pulverized or is difficult to crush, and thus the firing may be performed for
less than or equal to 10 h.
[0038] The firing may be performed under an air atmosphere, or under an inert gas atmosphere
such as nitrogen, argon, or the like depending on the composition or structure of
a manufactured compound. The resultant is preferably pressed.
[0039] The method of manufacturing a lithium-titanium composite oxide doped with different
metals according to the present invention may further include a step v) of pulverizing
the fired particles. The fired particles may be pulverized in a dry pulverizing method,
and the dry pulverization has no particular limit but may specifically be performed
by using a jet air mill to have a micrometer size.
[0040] Another embodiment of the present invention provides particles pulverized by the
additional dry-pulverizing step. In the present invention, the particles are primary
particles and have a weaker bond through the dry pulverization and separation, and
resultantly have a particle size D
50 ranging from 0.7 µm to 1.5 µm.
[0041] The present invention provides a lithium-titanium composite oxide doped with different
metals manufactured by the manufacturing method according to the present invention
and represented by the following chemical formula.
[Chemical Formula] Li
4Ti
5-(x+y)M)
xA
yO
12
(In the chemical formula, M is selected from the group consisting of Zr, Mg, Al, Ni,
Co, Mn, and Cu, the A is selected from the group consisting of Na, K, V, and B, 0.1≤x≤1.5,
0≤y≤1, x+y≤2, and 8≤x/y ≤9)
[0042] Each component of the lithium-titanium composite oxide doped with different metals
synthesized in the present invention may have a composition adjusted by a ratio of
each compound during the mixing, that is, a ratio of mixing of each compound. In addition,
powder characteristics such as particle distribution, BET specific surface area, tap
density, and pulverized powder density may be adjusted by a mixing method and an oxidation
treatment.
[0043] The lithium-titanium composite oxide doped with different metals of the present invention
includes secondary particles formed by aggregation of primary particles, wherein a
diameter of the primary particles ranges from 0.5 µm to 0.8 µm and a diameter of the
secondary particles ranges from 5 µm to 25 µm.
[0044] The lithium-titanium composite oxide doped with different metals manufactured according
to the manufacturing method of the present invention has a spinel structure. Particularly,
the lithium-titanium composite oxide doped with different metals manufactured according
to the manufacturing method of the present invention has a main peak intensity of
anatase-type TiO
2 of less than or equal to 1, a main peak intensity of R-TiO
2 of less than or equal to 1, and a main peak intensity of Li
2TiO
3 of less than or equal to 5 when a main peak intensity of Li
4/3Ti
5/3O
4 is 100.
[0045] The rutile-type titanium dioxide may show a main peak at 2θ = 27.4. The lithium-titanium
composite oxide doped with different metals manufactured in the manufacturing method
of the present invention includes the rutile-type titanium dioxide that deteriorates
capacity as an impurity but shows a main peak size of less than or equal to 1 and
is thus included in a very small amount, and accordingly, may increase battery capacity
as well as crystallinity.
[0046] The method of manufacturing the lithium-titanium composite oxide doped with different
metals according to the present invention may provide a titanium dioxide having excellent
capacity characteristics and structural characteristics by mixing, pulverizing, and
spray-drying different metals to dope two kinds of different metals on the surface
of a lithium-titanium composite oxide in an appropriate ratio and reduce the content
of conventional impurities such as rutile-type titanium dioxide, anatase-type titanium
dioxide, and Li
2TiO
3, and accordingly, a battery including the titanium dioxide doped with different metals
shows excellent battery characteristics such as high initial charge and discharge
efficiency and rate capability.
BRIEF DESCRIPTION OF THE DRAWINGS
[0047]
FIG. 1 is a SEM photograph showing a lithium-titanium composite oxide doped with one
kind of different metal according to one example of the present invention.
FIG. 2 shows capacity characteristics and rate capabilities of a test cell including
the lithium-titanium composite oxide doped with one kind of a different metal according
to one example of the present invention.
FIG. 3 is a SEM photograph showing a lithium-titanium composite oxide doped with two
kinds of different metals according to one example of the present invention.
FIG. 4 shows capacity characteristics and rate capabilities of a test cell including
the lithium-titanium composite oxide doped with two kinds of different metals according
to one example of the present invention.
FIG. 5 is an XRD photograph showing the lithium-titanium composite oxide doped with
two kinds of different metals according to one example of the present invention and
a lithium-titanium composite oxide according to a comparative example.
DETAILED DESCRIPTION
[0048] Hereinafter, embodiments of the present invention are described in detail. However,
these embodiments are exemplary, and this disclosure is not limited thereto.
<Example 1> Manufacture of Lithium-Titanium Composite Oxide Doped with One Kind of
a Different Metal
[0049] One mol of lithium hydroxide and 1 mol of an anatase-type titanium oxide as a starting
material are mixed with 0.1 mol of Zr as a different metal in a solid-phase, and they
are then stirred and dissolved in water.
[0050] Next, a lithium-titanium composite oxide was manufactured by pulverizing the mixture
using zirconia beads at 3000 rpm, spray-drying them at a hot air temperature of 270
°C and at a discharge hot air temperature of 120 °C, heat-treating them at two firing
temperatures of 750 °C and 770 °C for 10 hours under an oxygen atmosphere, and dry-pulverizing
them with a jet air mill.
[0051] Then, Al, Mg, and Na as different metals were respectively used in a ratio of 0.05
mol to manufacture each lithium-titanium composite oxide in the same method as above.
<Experimental Example 1-1> Measurement of SEM Photograph
[0052] FIG. 1 shows a SEM photograph showing each lithium-titanium composite oxide doped
with one kind of a different metal according to Example 1.
<Experimental Examples 1 and 2> Evaluation of Battery Characteristics - Measurement
of Capacity Characteristics and Rate Capability
[0053] The lithium-titanium composite oxide doped with one kind of a different metal according
to Example 1 as a positive active material, a lithium foil as a counter electrode,
and a porous polyethylene film (Celgard 2300 made by Celgard, LLC, thickness: 25 µm)
as a separator, and a liquid electrolyte solution obtained by mixing ethylene carbonate
and dimethyl carbonate in a volume ratio of 1:2 and dissolving LiPF
6 in a concentration of 1 mol in the mixed solvent were used according to a commonly-known
method, manufacturing a coin cell. A coin cell according to the comparative example
was manufactured according to the same method as above.
[0054] The capacity and rate capability of the test cell according to Comparative Example
1 including a lithium-titanium composite oxide doped with one kind of a different
metal were measured, and the results are provided in FIG. 2. Referring to FIG. 2,
the lithium-titanium composite oxide doped with Zr or Na turned out to improve the
capacity characteristic and rate capability compared with the lithium-titanium composite
oxide doped with Al or Mg.
<Example 2> Manufacture of Lithium-titanium Composite Oxide Doped with Two Kinds of
Different Metals
[0055] Each lithium-titanium composite oxide doped with two kinds of different metals such
as zirconium and sodium which showed an excellent capacity characteristic and rate
capability in Example 1 was manufactured.
[0056] Firstly, 1 mol of lithium hydroxide and 1 mol of anatase-type titanium oxide, and
0.05 mol of zirconium as a starting material, were mixed in a solid phase with a mixture
of sodium carbonate and sodium hydroxide as a sodium compound by changing their mol
ratios to 0.006, 0.008, and 0.01, and the mixture was stirred and dissolved in water.
[0057] The solution was wet-pulverized with zirconia beads at 3000 rpm, spray-dried at a
hot-air temperature of 270 °C and at a discharge hot-air temperature of 120 °C, respectively
heat-treated at 750 °C and 770 °C for 10 h under an oxygen atmosphere, and dry-ground
with a jet air mill, manufacturing a lithium-titanium composite oxide doped with two
kinds of different metals.
<Experimental Example 2-1> SEM Photograph Measurement
[0058] SEM photographs of particles of the lithium-titanium composite oxide doped with two
kinds of different metals according to Example 2 and a lithium-titanium composite
oxide doped with only Zr in an amount of 0.05 mol are provided in FIG. 3. When two
kinds of different metals were doped in FIG. 3, the particle size was not changed.
[0059] FIG. 4 shows the results of the primary particle size of the lithium-titanium composite
oxide doped with two kinds of different metals according to Example 2. The primary
particle size was in a range of 0.564 to 0.757 um.
<Experimental Example 2-2> Electrochemical Characteristics
[0060] The lithium-titanium composite oxide doped with two kinds of different metals according
to Example 2 as a positive active material, a lithium foil as a counter electrode,
a porous polyethylene film (thickness: 25 µm, Celgard 2300, Celgard LLC.) as a separator,
and a liquid electrolyte solution prepared by mixing ethylene carbonate and dimethyl
carbonate in a volume ratio of 1:2 and dissolving LiPF
6 in a concentration of 1 mol were used to manufacture a coin cell in a commonly-known
method. A coin cell according to the comparative example was manufactured according
to the same method as above.
[0061] The capacity and rate capability of a test cell including the lithium-titanium composite
oxide doped with two kinds of different metals according to Example 2 were measured,
and the results are provided in FIG. 5. Referring to FIG. 5, the cells using lithium-titanium
composite oxides respectively doped with two kinds of different metals of Zr and Na
in an amount of 0.05 mol and 0.006 mol and heat-treating them at 750 °C according
to the examples showed superior improvement rate capabilities compared with the cell
using the lithium-titanium composite oxide according to the comparative example.
<Experimental Example 2-3> XRD Measurement
[0062] FIG. 6 shows the lithium-titanium composite oxides respectively doped with two kinds
of different metals of Zr and Na in an amount of 0.05 mol and 0.006 mol and heat-treated
at 750 °C according to the examples and the lithium-titanium composite oxide not doped
with different metals according to the comparative example.
[0063] Referring to FIG. 6, the lithium-titanium composite oxides doped with two kinds of
different metals of Na and Zr according to one example of the present invention had
a spinel structure, and when Li
4/3Ti
5/3O
4 has a main peak intensity of 100, anatase-type TiO
2 had a main peak intensity of less than or equal to 1, rutile-type TiO
2 had a main peak intensity of less than or equal to 1, and Li
2TiO
3 had main peak intensity of less than or equal to 5. Battery performance turned out
to be improved by controlling the content of impurities such as anatase-type titanium
dioxide, rutile-type titanium dioxide, and Li
2TiO
3 doped with the Na and Zr as different metals and the like.
1. A manufacturing method of a lithium-titanium composite oxide doped with different
metals, comprising:
i) solid-phase stoichiometrically mixing a lithium-containing compound, a titanium
oxide, a different metal M-containing compound, and a different metal A-containing
compound;
ii) dispersing the solid-phase mixture of the i) in a solvent and wet-pulverizing
the mixture to have particles having an average particle diameter of 0.3 µm to 0.8
µm to prepare a slurry;
iii) spray-drying the slurry to provide particles; and
iv) firing the spray-dried particles to manufacture a lithium-titanium composite oxide
doped with different metals represented by the following chemical formula:
[Chemical Formula] Li4Ti5-(x+y)MxAyO12
(in the chemical formula, the M is selected from the group consisting of Zr, Mg, Al,
Ni, Co, Mn, and Cu, the A is selected from the group consisting of Na, K, V, and B,
0.1≤x≤1.5, 0≤y≤1, x+y≤2, and 8≤x/y ≤9).
2. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 1, wherein the different metal M is Zr and the different metal A is
Na.
3. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 2, wherein the Zr-containing compound is Zr(OH)4, ZrO2, or a mixture thereof.
4. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 2, wherein the Na-containing compound is selected from the group consisting
of sodium carbonate, sodium hydroxide, sodium carbonate, and sodium hydroxide.
5. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 1, wherein the titanium oxide is an anatase-type, or a titanium oxide
hydrate.
6. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 1, wherein the lithium-containing compound is lithium hydroxide or
lithium carbonate.
7. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 1, wherein in the ii) process, water is used as a solvent, and the
wet-pulverizing is performed using zirconia beads at 2000 to 4000 rpm.
8. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 1, wherein in the iii) process, the spray drying is performed while
inflowing hot air at a temperature of 250 to 300 °C and discharging hot air at a temperature
of 100 to 150 °C.
9. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 1, wherein in the iv) process, the firing is performed by firing the
spray-dried resultant of the iii) process at an air atmosphere at 700 to 800 °C for
5 h to 10.
10. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 1, wherein the method further comprises v) pulverizing the fired particles
in the iv) process.
11. The manufacturing method of a lithium-titanium composite oxide doped with different
metals of claim 10, wherein the v) fired particles are pulverized using a jet air
mill.
12. A lithium-titanium composite oxide doped with different metals manufactured by the
method of any one of claim 1 to claim 11, comprising secondary particles formed by
aggregating primary particles, having a spinel structure, and represented by the following
chemical formula, wherein a diameter of the primary particles ranges from 0.5 µm to
0.8 µm and a diameter of the secondary particles ranges from 5 µm to 25 µm:
[Chemical Formula] Li4Ti5-(x+y)MxAyO12
(in the chemical formula, the M is selected from the group consisting of Zr, Mg, Al,
Ni, Co, Mn, and Cu, the A is selected from the group consisting of Na, K, V, and B,
0.1≤x≤1.5, 0≤y≤1, x+y≤2, and 8≤x/y≤9).
13. The lithium-titanium composite oxide doped with different metals of claim 12, wherein
the secondary particles have D50 of 0.7 µm to 1.5 µm.
14. The lithium-titanium composite oxide doped with different metals of claim 12, wherein
the lithium-titanium composite oxide doped with different metals has a main peak intensity
of anatase-type TiO2 of less than or equal to 1, a main peak intensity of R-TiO2 of less than or equal to 1, and a main peak intensity of Li2TiO3 of less than or equal to 5 when a main peak intensity of Li4/3Ti5/3O4 is 100.
15. A positive electrode for a rechargeable lithium battery comprising the lithium-titanium
composite oxide doped with different metals of claim 12.
16. A negative electrode for a rechargeable lithium battery comprising the lithium-titanium
composite oxide doped with different metals of claim 12.
17. A rechargeable lithium battery comprising the positive electrode of claim 15.
18. A rechargeable lithium battery comprising the negative electrode of claim 16.